• KSCE Journal of Civil and Environmental Engineering Research
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• v.5 no.4
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• pp.45-56
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• 1985

This study was made to evaluate temperature effects on biological wastewater treatment particularly at the lower temperatures. Cell yield coefficients and other kinetic factors were compared by varying temperature for industrial wastes. Bench scale aeration-only complete mixing activated sludge(CMAS) units were operated at temperatures of $1^{\circ}$, $4^{\circ}$, $7^{\circ}$ and $10^{\circ}C$ with substrate concentrations of 5,000 and 200 mg/l COD. The study results indicate that the cell yields were computed to be 0.5 to 0.6 grams VSS per grams BOD removed, and were not influenced by temperature variations. The synthesis/total energy ratios were computed to be 0.45 to 0.58 and had a tendency to become larger at lower temperatures. The endogenous respiration rates were computed to be 0.07 to 0.08/day, and seemed to be independent of temperature. In addition, very little temperature effects were observed when F/M ratio and substrate concentrations were reduced.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.11
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• pp.1180-1185
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• 2005

Iron sand, having iron as a major component, was applied in the treatment of synthetic wastewater containing Cu(II) or Pb(II). To investigate the stability of iron sand at acidic condition, dissolution of Fe and Al was studied with variation of solution pH ranging from 2 to 4.5. Iron concentration in the extracted solution was below the emission regulation of wastewater even at a strong acidic condition, pH 2. Although an important concentration of aluminum was extracted at pH 2, the dissolution greatly decreased above pH 3. This stability test suggests that application of iron sand has little problem in the treatment of wastewater above pH 3. Adsorption capacity of Cu(II) and Pb(II) onto iron sand was investigated in a batch and a column test. In case of Cu(II), rapid adsorption was noted, showing 50% removal within 2 hrs, and then reached a near complete equilibrium after 24 hrs. Adsorption was favorable at higher pH in each metal ion and showed a near complete removal above pH 6, indicating a typical cationic-type adsorption. From the adsorption isotherm obtained with variation of the concentration of each metal ion, the maximum adsorption capacity of Cu(II) and Pb(II) was identified as 2,170 mg/kg 및 3,450 mg/kg, respectively.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.12 no.9
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• pp.4274-4282
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• 2011

In this study, Fenton reaction was studied for the possibility of applying as advanced treatment and its optimal condition for the removal of refractory organics from the dye wastewater. Fenton reaction was applied to remove refractory organics after the bio-treatment (secondary treatment) inside test laboratory and on-site pilot plant. Wastewater from the secondary treatment was used and its $COD_{Mn}$ was measured as 30~50mg/L. After the Fenton reaction, the optimal condition was found as pH 3~3.5, reaction time 2~2.5hr, chemical input ratio of ($FeCl_2$(33%)/$H_2O_2$(35%)) was 3 : 1. When chemical input ratio of ($FeCl_2$(33%)/$H_2O_2$(35%)) was at its optimal, amount of sludge volume ($SV_{2hr}$) was 21~28%. With pilot plant test, removal rate was heavily influenced by the hydraulic retention time(HRT), and optimum value of HRT was 2.0 hr. When pilot plant($2m^3/d$) was placed on-site and operated continuously, it showed steady and fairly good treatment of COD where COD removal rate was 60~70%, treated water showed below 20mg/L.

• 한국생물공학회:학술대회논문집
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• 2001.11a
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• pp.568-571
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• 2001

Food wastewater eluted from the three-stage methane fermentation system developed in this lab showed high concentrations of TCOD, BOD, T-N and T-P. Because the effluent of biological filter chamber (BFC) still had high concentration of nitrogen and organic material, the effluent was treated with algal periphyton system using algae. The removal rates of COD, T-N and T-P wer 96, 98 and 91%, respectively, in this system. The grown algae could digested byy waterfleas using the ecological food chain system. Food wastewater is better than algal culture medium for growth of waterflea, Moima Macrocopa. During 12days, the individual of waterflea increased to 180 in the food wastewater containing a T-N concentration of 150 mg/ ${\ell}$.

• 한국생물공학회:학술대회논문집
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• 2001.11a
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• pp.549-551
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• 2001

The heavy use of petroleum products in modern livings has brought ubiquitous environmental contaminants of aromatic compounds, which persist in aquatic and geo-environment without the substantial degradation. The persistence and accumulation of the aromatic compounds, which include xylene, phenol, toluene, phthalate, and so on are known to cause serious problems in our environments. Some of soil and aquatic microorganisms facilitate their growth by degrading aromatic compounds and utilizing degrading products as growth substrates, the biodegradation helps the reentry of carbons of aromatic compounds, preventing their accumulation in our environments. The metabolic studies on the degradation of aromatic compounds by microoganisms were extensively carried out along with their genetic studies. A Rhodococcus sp. EL-GT isolated in activated sludges has shown the excellent ability to grow on phenol as a sole carbon source. In the present study investigated a gene encoding phenol-degrading enzymes from a Rhodococcus sp. EL-GT.

• Proceedings of the Korea Technical Association of the Pulp and Paper Industry Conference
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• 2001.11a
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• pp.141-141
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• 2001

사이즈 프레스용 전분은 주로 산화전분이 이용되고 있으며, 전분업체에서 공급되는 것과 제지공장에서 자가변성으로 제조하여 이용하는 것으로 나눌 수 있다. 자가변성의 경우 경제적 측면에서 원가절감이 가능한 장점이 있는 반면 전분 품질이 다소 미흡한 단점이 있다. 자가변성 산화제로는 APSCAmmonium persulfate), 효소 등이 이용된다. 효소는 APS에 비해 전분 분자 내의 1,4결합만을 가수분해 시키고 점도안정성과 전분 용액 색상이 양호한 특성을 보인다. 또한 온도/농도/점도 등의 상관성을 자유롭게 이용하여 요구하는 전분 용액 품질을 얻을 수 있다. 제지용 전분 산화용으로는 주로 알파 -아밀라아제가 이용된다.본 실험은 산화전분을 효소변성을 이용한 생전분으로 가능성을 알아보고자 진행되었다. 일차적으로 실험실에서 하였고, 몇 차례의 mill trial을 통해 효소변성 전분 적용을 최적화하고자 하였다. 실험실적으로 효소변성을 위한 반응조건으로 온도, 시간, pH, 투입량 등을 설정하였 고, 각 조건별로 제조된 전분 용액의 점도를 측정하여 효소 반응성을 평가하였다. 실험 결과 전분 용액의 점도는 낮았고, 점도 안정성 또한 양호한 수준을 보였다. Cooking농 도는 20%로 하였으나 보다 고농도 cooking의 가능성을 확인할 수 있었다. 시트 물성도 전반적으로 산화전분 대비 대등한 수준을 나타내었다. Mill trial은 무림제지에서 실시하였고 사이즈 프레스 조제식을 이용하였다. 전분 농도는 초기에 20%로 시작하여 30%까지 올려서 trial을 실시하 였고, 그 외 작업조건들은 산화전분 적용 시와 동일하게 하였다. 효소 반응시간으로 인해 cooking시간이 다소 많이 걸렸으나 전반적인 조제 작업은 큰 문제 없이 이루어졌고, 효소변성 전분 용액의 점도는 낮은 수준으로 유지되었다. 사이즈 프레스 작업성이나 시 트 물성도 산화전분 적용 시와 대등한 수준을 보였으나, 전분 차이로 인한 색상 차이로 부가적인 염료 조정이 이루어졌다. 한편 폐수부하 증가를 우려하였으나, 이에 따른 문제는 크게 발생되지 않았다.

• Proceedings of the Korea Water Resources Association Conference
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• 2005.05b
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• pp.1234-1238
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• 2005

우리나라의 수질오염에 대한 규제는 주로 호소 및 하천의 수질을 향상시키기 위하여 하수 및 공장폐수 등 점오염원을 중심으로 관리되어 왔으나 강우와 함께 대량 유출된 비점오염원은 수용하천의 자정능력을 감소시키고 있고 이로 인해 하천과 호소의 수질은 향상되지 못하고 있다. 또한, 농촌지역에서 배출되는 비점오염원은 정확한 기작의 분석이 안 되고 있으며, 비료$\cdot$농약의 사용 증가에 따라 영양염 및 유해물질에 의한 수질오염의 영향이 증가되고 있는 실정이다. 본 연구는 농촌지역의 강우-유출로 인한 비점오염물질의 유출특성 및 배출부하량을 조사하기 위하여 영산강권역의 외남천을 대상으로 조사하였다. 대상 유역의 토지용도 구분은 (1)논지역, (2)밭지역, (3)산지지역, (4)농촌주거지역, (5)복합지역(논, 산지)으로 구분하였다. 시료의 채취는 강우시 5회에 걸쳐 조사하였으며, 2L 용량의 무균채수병에 채취한 후, 아이스박스에 $4^{\circ}C$이하로 보관하여 24시간 이내로 실험실에 운반하여 실험하였으며, 매회 시료 채취 주기는 강우유출이 발생하기 전부터 강우 종료 후 유출량 변화가 없을 때까지 $9\~12$단계로 세분하여 유출량과 pH, DO, BOD, COD, SS, T-N, T-P의 농도를 측정하였다. 본 연구에서 조사한 결과 토지이용별 비점오염원의 SMC를 살펴보면 BOD의 SMC는 $4.38\~11.02mg/{\ell}$, COD의 SMC는 $7.07\~23.99mg/{\ell}$, T-N은 $1.57\~5.20mg/{\ell}$, T-P는 $0.11\~0.274mg/{\ell}$의 범위를 갖는 것으로 나타났으며, 전반적으로 논 지역에서 비교적 높게 나타났는데 이는 농작물의 경작에 따른 시비법의 영향으로 판단된다. 또한, 비점오염원의 유출특성을 보면 전반적으로 초기 오염물질 유출특성 갖는 것으로 나타났다.

• Journal of Korean Society of Environmental Engineers
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• v.37 no.6
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• pp.363-370
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• 2015

The production of polyhydroxyalkanoates (PHAs) using Sequencing Batch Reactor (SBR) was investigated. The experiments were performed in two fabricated SBRs (4 L) of different oxidation state. Synthetic wastewater was used as substrate, using C/N/P ratio of 42:10:1. SBR 1 and SBR 2 were operated in aerobic dynamic feeding (ADF) and anaerobic/oxic dynamic feeding (AODF) condition, respectively. ADF provide feast and famine in aerobic condition, while AODF in anaerobic/oxic condition. PHAs production was found high in AODF than AOF. Maximum PHAs content of 40.0% (w/w)of biomass were produced in AODF mode. Produced PHAs structural and thermal property were good.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1993.05a
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• pp.33-41
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• 1993

The objectives of this experiment performed were to determine the potential using of solar radiation to destroy organic contaminants in water by photolysis and to develop the process and improve its performance. We used lab, scale of recirculation photoreactor with 30, 50, 80ppm initial concentration of TCE and Ti $O_2$ anatase, respectively. Adsorption constant, reaction constant were obtained and compared using the Langmuir-Hinshelwood kinetics equation. Ti $O_2$ anatase demonstrated the highest conversion ratio co TCE among Ti $O_2$ anatase, ZnO and F $e_2$ $O_3$ in this experiment. It was shown that in case of two component system, TCE+ phenol, as the concentration of phenol increased in the feed solution, TCE decomposition rate decreased.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.8 no.2
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• pp.77-88
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• 1988

This research investigated the effect of COD/N ratio on nitrogen removal, and the use of organics in raw wastewater as a carbon source for denitrification in SBR(Sequencing Batch Reactor) systems. Four laboratory scale reactors were operated in three modes. Only the difference between modes were; Mode I operated in aerated condition during fill while Mode II in anoxic condition and Mode III operated on two fills per cycle in anoxic condition. When COD/N ratio increased, total nitrogen removal efficiencies increased from 8.7 to 57.7 percent in Mode I, from 28.9 to 83.2 percent in Mode II and from 42.7 to 97.8 percent in Mode III, respectively. COD removal efficiencies ranged from 93 to 98 percent throughout the study. SBR operation in Mode III of feeding twice per cycle in anoxic condition was an effective operating method for nitrogen removal and nitrogen concentration in effluent can be estimated using influent COD and nitrogen concentrations.